CA2976131C - Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases - Google Patents
Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases Download PDFInfo
- Publication number
- CA2976131C CA2976131C CA2976131A CA2976131A CA2976131C CA 2976131 C CA2976131 C CA 2976131C CA 2976131 A CA2976131 A CA 2976131A CA 2976131 A CA2976131 A CA 2976131A CA 2976131 C CA2976131 C CA 2976131C
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- Prior art keywords
- filter
- gas
- scr
- exhaust gas
- engine exhaust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000007789 gas Substances 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000000919 ceramic Substances 0.000 title claims abstract description 19
- 238000004140 cleaning Methods 0.000 title description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000003054 catalyst Substances 0.000 claims abstract description 30
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 27
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 16
- 230000003647 oxidation Effects 0.000 claims abstract description 15
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 15
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 11
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 11
- 239000013618 particulate matter Substances 0.000 claims abstract description 11
- 229910001935 vanadium oxide Inorganic materials 0.000 claims abstract description 10
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000004071 soot Substances 0.000 claims abstract description 8
- 239000006185 dispersion Substances 0.000 claims abstract description 6
- 239000002956 ash Substances 0.000 claims abstract description 5
- 229910052751 metal Inorganic materials 0.000 claims abstract description 5
- 239000002184 metal Substances 0.000 claims abstract description 5
- 150000002736 metal compounds Chemical class 0.000 claims abstract description 5
- 150000002739 metals Chemical class 0.000 claims abstract description 5
- 239000000835 fiber Substances 0.000 claims description 10
- FGZBFIYFJUAETR-UHFFFAOYSA-N calcium;magnesium;silicate Chemical compound [Mg+2].[Ca+2].[O-][Si]([O-])([O-])[O-] FGZBFIYFJUAETR-UHFFFAOYSA-N 0.000 claims description 5
- 229910010293 ceramic material Inorganic materials 0.000 claims description 5
- 239000003638 chemical reducing agent Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 5
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 4
- 235000012241 calcium silicate Nutrition 0.000 claims description 3
- 239000000378 calcium silicate Substances 0.000 claims 2
- 229910052918 calcium silicate Inorganic materials 0.000 claims 2
- 229960003340 calcium silicate Drugs 0.000 claims 2
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- 239000012855 volatile organic compound Substances 0.000 description 6
- 239000010936 titanium Substances 0.000 description 5
- 239000011149 active material Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 3
- -1 NON Substances 0.000 description 2
- 230000010718 Oxidation Activity Effects 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910021541 Vanadium(III) oxide Inorganic materials 0.000 description 2
- 229910021542 Vanadium(IV) oxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000002013 dioxins Chemical class 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 2
- IBYSTTGVDIFUAY-UHFFFAOYSA-N vanadium monoxide Chemical compound [V]=O IBYSTTGVDIFUAY-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 239000011865 Pt-based catalyst Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229960000510 ammonia Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- JHLNERQLKQQLRZ-UHFFFAOYSA-N calcium silicate Chemical class [Ca+2].[Ca+2].[O-][Si]([O-])([O-])[O-] JHLNERQLKQQLRZ-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 150000002240 furans Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- KFAFTZQGYMGWLU-UHFFFAOYSA-N oxo(oxovanadiooxy)vanadium Chemical compound O=[V]O[V]=O KFAFTZQGYMGWLU-UHFFFAOYSA-N 0.000 description 1
- DUSYNUCUMASASA-UHFFFAOYSA-N oxygen(2-);vanadium(4+) Chemical compound [O-2].[O-2].[V+4] DUSYNUCUMASASA-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- GRUMUEUJTSXQOI-UHFFFAOYSA-N vanadium dioxide Chemical compound O=[V]=O GRUMUEUJTSXQOI-UHFFFAOYSA-N 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Classifications
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
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- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8643—Removing mixtures of carbon monoxide or hydrocarbons and nitrogen oxides
- B01D53/8646—Simultaneous elimination of the components
- B01D53/865—Simultaneous elimination of the components characterised by a specific catalyst
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- B01D53/34—Chemical or biological purification of waste gases
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- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
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- B01D53/8656—Successive elimination of the components
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- B01D53/9413—Processes characterised by a specific catalyst
- B01D53/9418—Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
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- B01D53/944—Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
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- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
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- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
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- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/022—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous
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- F01N3/033—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
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- F01N3/105—General auxiliary catalysts, e.g. upstream or downstream of the main catalyst
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- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2066—Selective catalytic reduction [SCR]
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2370/00—Selection of materials for exhaust purification
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Abstract
Ceramic candle filter and use of the filter in the removal of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst arranged at least on the dispersion side and/or with in wall of the filter, the combined SCR and oxidation catalyst comprises palladium, a vanadium oxide and titania.
Description
Title: Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases The present invention relates to ceramic candle filters and a method for cleaning of off- or exhaust gases. More par-ticularly, the invention provides a catalyzed ceramic can-dle filter for the removal of dust and particulate matter in a process gas and harmful components contained in the process gas. The catalyzed ceramic candle filter is in par-ticular useful in the cleaning of process or raw gas from industrial processes involving combustion, like the produc-tion of minerals, glass, cement, waste incineration, or from coal fired boilers and engines.
Ceramic filters in form of filter candles are used in many industries for removal of particulate matter from process gases. They are one of the most efficient types of dust collectors available and can achieve collection efficien-cies of more than 99% for particulates. The filters can be made from various ceramic materials comprising ceramic fi-bres made of alkali and alkaline earth silicates, or alumi-no silicates.
The high particulate removal efficiency of ceramic candle filters is partly due to the dust cake formed on the sur-faces of the candle filter and partly due to the candle filter composition and porosity. In order to provide suffi-cient filtration activity and an acceptable low pressure drop over the filter conventional ceramic candle filters have a porosity of between 70 and 90%. The wall thickness of those filters should be in the range of 10-20 mm for sufficient stability and mechanical strength.
Ceramic filters in form of filter candles are used in many industries for removal of particulate matter from process gases. They are one of the most efficient types of dust collectors available and can achieve collection efficien-cies of more than 99% for particulates. The filters can be made from various ceramic materials comprising ceramic fi-bres made of alkali and alkaline earth silicates, or alumi-no silicates.
The high particulate removal efficiency of ceramic candle filters is partly due to the dust cake formed on the sur-faces of the candle filter and partly due to the candle filter composition and porosity. In order to provide suffi-cient filtration activity and an acceptable low pressure drop over the filter conventional ceramic candle filters have a porosity of between 70 and 90%. The wall thickness of those filters should be in the range of 10-20 mm for sufficient stability and mechanical strength.
2 Particle-containing process off-gas and engine exhaust gas often contains a plurality of pollutants, e.g. NON, vola-tile organic compounds (VOC), SO2, CO, NH3, dioxins and fu-rans, in concentrations that have to be reduced depending on local legislation. For this purpose, several convention-al methods are available. The abatement of gaseous contami-nants like NON, VOC, dioxins and furans can be effectively carried out by contact with a catalyst. In particular, va-nadium oxide-based catalysts are commonly used catalysts for NOõ reduction by selective reduction of NO, with NH3 in stationary and automotive applications.
This catalyst is active both in the oxidative removal of hydrocarbons (VOC) and in the selective catalytic reduction (SCR) of NOx by reaction with NH3.
In comparison to the precious metal catalysts, like the Pd catalyst, the vanadium oxide catalyst is less selective in the formation of CO2 and some amounts of CO are produced during the oxidation reactions. CO cannot be oxidized to 002 at a feasible reaction rate by contact with the vanadi-um oxide catalyst.
We have found that when providing the candle filter with a catalyst comprising both vanadium oxide and palladium re-sults in an effective oxidation of hydrocarbons and soot together with ammonia-SCR of NOx and a lower slip of ammo-nia and carbon monoxide from the filter.
Pursuant to this finding, the present invention provides
This catalyst is active both in the oxidative removal of hydrocarbons (VOC) and in the selective catalytic reduction (SCR) of NOx by reaction with NH3.
In comparison to the precious metal catalysts, like the Pd catalyst, the vanadium oxide catalyst is less selective in the formation of CO2 and some amounts of CO are produced during the oxidation reactions. CO cannot be oxidized to 002 at a feasible reaction rate by contact with the vanadi-um oxide catalyst.
We have found that when providing the candle filter with a catalyst comprising both vanadium oxide and palladium re-sults in an effective oxidation of hydrocarbons and soot together with ammonia-SCR of NOx and a lower slip of ammo-nia and carbon monoxide from the filter.
Pursuant to this finding, the present invention provides
3 a ceramic candle filter suitable for the removal of partic-ulate matter in form of soot, ash, metals and metal com-pounds, together with hydrocarbons and nitrogen oxides be-ing present in process off-gas or engine exhaust gas, the filter comprises a combined SCR and oxidation catalyst ar-ranged at least on the dispersion side and/or within wall of the filter, the combined SCR and oxidation catalyst com-prises palladium, a vanadium oxide and titania.
The terms "dispersion side" and "permeate side" as used herein refer to the flow side of the filter facing the un-filtered exhaust gas and to flow side facing the filtered off- or exhaust gas, respectively.
The invention provides additionally a method for the remov-al of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, comprising the steps of providing a process off-gas or engine exhaust gas contain-ing a nitrogenous reductant or adding the nitrogenous re-ductant to the off- or exhaust gas;
passing the off-gas or the exhaust through a ceramic candle filter and capturing the particulate matter; and reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off- or exhaust gas by oxidation of the hydrocarbons and by selective cata-lytic reduction (SCR) of the nitrogen oxides with the ni-trogenous reductant in contact with a combined SCR and oxi-dation catalyst being arranged on the dispersion side and/or within wall of the filter, wherein the combined SCR
The terms "dispersion side" and "permeate side" as used herein refer to the flow side of the filter facing the un-filtered exhaust gas and to flow side facing the filtered off- or exhaust gas, respectively.
The invention provides additionally a method for the remov-al of particulate matter in form of soot, ash, metals and metal compounds, together with hydrocarbons and nitrogen oxides being present in process off-gas or engine exhaust gas, comprising the steps of providing a process off-gas or engine exhaust gas contain-ing a nitrogenous reductant or adding the nitrogenous re-ductant to the off- or exhaust gas;
passing the off-gas or the exhaust through a ceramic candle filter and capturing the particulate matter; and reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off- or exhaust gas by oxidation of the hydrocarbons and by selective cata-lytic reduction (SCR) of the nitrogen oxides with the ni-trogenous reductant in contact with a combined SCR and oxi-dation catalyst being arranged on the dispersion side and/or within wall of the filter, wherein the combined SCR
4 and oxidation catalyst comprises palladium, a vanadium ox-ide and titania.
The term "a vanadium oxide" or "vanadium oxide" refers to:
Vanadium(II)oxide (vanadium monoxide), VO; or vanadium(III)oxide (vanadium sesquioxide or trioxide), V203; or vanadium(IV)oxide (vanadium dioxide), V02; or vanadium(V)oxide (vanadium pentoxide), V205.
Preferably, vanadium oxide for use in the invention com-prises or consists of vanadium(V)oxide (vanadium pentox-ide), V205.
The term "titania" refers to titanium dioxide (Ti02).
The catalytically active form of palladium is palladium in the metallic and/or oxidic form.
The shortage Pd/V/Ti shall mean a catalyst consisting of palladium, a vanadium oxide and titania.
The Pd/V/Ti catalyst has i) dual functionality (removal of NOx and removal of VOC, volatile organic compounds); ii) a S-tolerance; and iii) a lower SO2 oxidation activity com-pared to other catalyst compositions, e.g. Pt-based cata-lysts.
When employing a Pd/V/Ti catalyst the catalyzed filter can-dles are sulfur resistant, i.e. not subjected to sulfur de-activation. The Pd/V/Ti catalyst additionally reduces the amount of SO3 formed by oxidation of SO2. If H2S is also
The term "a vanadium oxide" or "vanadium oxide" refers to:
Vanadium(II)oxide (vanadium monoxide), VO; or vanadium(III)oxide (vanadium sesquioxide or trioxide), V203; or vanadium(IV)oxide (vanadium dioxide), V02; or vanadium(V)oxide (vanadium pentoxide), V205.
Preferably, vanadium oxide for use in the invention com-prises or consists of vanadium(V)oxide (vanadium pentox-ide), V205.
The term "titania" refers to titanium dioxide (Ti02).
The catalytically active form of palladium is palladium in the metallic and/or oxidic form.
The shortage Pd/V/Ti shall mean a catalyst consisting of palladium, a vanadium oxide and titania.
The Pd/V/Ti catalyst has i) dual functionality (removal of NOx and removal of VOC, volatile organic compounds); ii) a S-tolerance; and iii) a lower SO2 oxidation activity com-pared to other catalyst compositions, e.g. Pt-based cata-lysts.
When employing a Pd/V/Ti catalyst the catalyzed filter can-dles are sulfur resistant, i.e. not subjected to sulfur de-activation. The Pd/V/Ti catalyst additionally reduces the amount of SO3 formed by oxidation of SO2. If H2S is also
5 present in the process gas entering the filter, it will also be oxidized to SO2 on the Pd/V/Ti catalyst.
The catalytically active material may be applied on the ceramic filter by impregnation with a slurry containing the catalytically active material in form of titania micro-particles and the precursors of the active materials, i.e. salts of vanadium and palladium. Once impregnated, the filter is subsequently dried and heated up to the required temperature for the decomposition of all precursors and activation of the catalyst.
Compared to monolithic formed filters or wall flow filters, the effective gas contact between the palladium metal particles and reactants in gas is much higher, which results in a much reduced amount of palladium necessary to obtain a reasonable oxidation activity.
Typically, the catalyst employed in the invention the catalyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably less than 200 ppm/weight.
In the case of high temperature ceramic filters several types of fibers may be used for their production. These can be constituted e.g. by silica-aluminate, calcium-magnesium-silicates, calcium-silicates fibers, or a mixture thereof.
Other preferred ceramic fibres comprise bio-soluble fibres selected from the group of calcium-magnesium-silicates.
Date recue/Date Received 2020-09-23
The catalytically active material may be applied on the ceramic filter by impregnation with a slurry containing the catalytically active material in form of titania micro-particles and the precursors of the active materials, i.e. salts of vanadium and palladium. Once impregnated, the filter is subsequently dried and heated up to the required temperature for the decomposition of all precursors and activation of the catalyst.
Compared to monolithic formed filters or wall flow filters, the effective gas contact between the palladium metal particles and reactants in gas is much higher, which results in a much reduced amount of palladium necessary to obtain a reasonable oxidation activity.
Typically, the catalyst employed in the invention the catalyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter, preferably less than 200 ppm/weight.
In the case of high temperature ceramic filters several types of fibers may be used for their production. These can be constituted e.g. by silica-aluminate, calcium-magnesium-silicates, calcium-silicates fibers, or a mixture thereof.
Other preferred ceramic fibres comprise bio-soluble fibres selected from the group of calcium-magnesium-silicates.
Date recue/Date Received 2020-09-23
Claims (6)
1. A ceramic candle filter suitable for the removal of particulate matter in the form of soot, ash, metals, and metal compounds, together with hydrocarbons and nitrogen oxides from process off-gas or engine exhaust gas, the filter comprising a combined selective catalytic reduction (SCR) and oxidation catalyst arranged at least on the dispersion side of the filter facing unfiltered gas and/or within a wall of the filter, the combined SCR and oxidation catalyst comprising palladium, a vanadium oxide and titania, wherein the ceramic material of the filter is produced from fibers selected from the group consisting of silica-aluminate fibers, calcium-magnesium-silicate fibers, calcium-silicate fibers, and mixtures thereof.
2. The ceramic candle filter of claim 1, wherein the catalyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter.
3. The ceramic candle filter according to claim 1 or 2, wherein the ceramic material of the filter consists of calcium-magnesium-silicate fibres that are bio-soluble.
4. A method for the removal of particulate matter in the form of soot, ash, metals, and metal compounds, together with hydrocarbons and nitrogen oxides from process off-gas or engine exhaust gas, comprising the steps of:
providing a process off-gas or engine exhaust gas containing a nitrogenous reductant or adding the nitrogenous reductant to the off-gas or the engine exhaust gas;
Date Recue/Date Received 2021-02-12 passing the off-gas or the engine exhaust gas through a ceramic candle filter and capturing the particulate matter;
and reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off-gas or engine exhaust gas by oxidation of the hydrocarbons and by selective catalytic reduction (SCR) of the nitrogen oxides with the nitrogenous reductant in contact with a combined SCR
and oxidation catalyst being arranged on the dispersion side of the filter facing unfiltered gas and/or within a wall of the filter, wherein the combined SCR and oxidation catalyst comprises palladium, a vanadium oxide and titania;
wherein the ceramic material of the filter is produced from fibers selected from the group consistin.g of silica-aluminate fibers, calcium-magnesium-silicate fibers, calcium-silicate fibers, and mixtures thereof.
providing a process off-gas or engine exhaust gas containing a nitrogenous reductant or adding the nitrogenous reductant to the off-gas or the engine exhaust gas;
Date Recue/Date Received 2021-02-12 passing the off-gas or the engine exhaust gas through a ceramic candle filter and capturing the particulate matter;
and reducing amounts of soot in the particulate matter captured on the at least one particulate filter and reducing amounts of nitrogen oxides and hydrocarbons in the off-gas or engine exhaust gas by oxidation of the hydrocarbons and by selective catalytic reduction (SCR) of the nitrogen oxides with the nitrogenous reductant in contact with a combined SCR
and oxidation catalyst being arranged on the dispersion side of the filter facing unfiltered gas and/or within a wall of the filter, wherein the combined SCR and oxidation catalyst comprises palladium, a vanadium oxide and titania;
wherein the ceramic material of the filter is produced from fibers selected from the group consistin.g of silica-aluminate fibers, calcium-magnesium-silicate fibers, calcium-silicate fibers, and mixtures thereof.
5. The method according to claim 4, wherein the combined oxidation and SCR catalyst contains palladium in an amount of between 20 and 1000 ppm/weight of the filter.
6. The method according to claim 4 or 5, wherein the ceramic material of the filter comprises calcium-maghesium-silicate fibres that are bio-soluble.
Date Recue/Date Received 2021-02-12
Date Recue/Date Received 2021-02-12
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JP6215361B2 (en) * | 2013-02-14 | 2017-10-18 | ハルドール・トプサー・アクチエゼルスカベット | Method and catalyst for simultaneous removal of carbon monoxide and nitrogen oxides from flue gas or exhaust gas |
DK3271049T3 (en) * | 2015-03-20 | 2020-04-27 | Haldor Topsoe As | Catalyzed ceramic core filter and process for purifying process flue gas or exhaust gas |
KR102454125B1 (en) | 2015-03-20 | 2022-10-14 | 토프쉐 에이/에스 | Catalyzed Ceramic Candle Filters and Methods for Purification of Process Offgases or Exhaust Gases |
US10105682B2 (en) * | 2015-03-20 | 2018-10-23 | Haldor Topsøe A/S | Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases |
KR20180009739A (en) * | 2015-05-19 | 2018-01-29 | 할도르 토프쉐 에이/에스 | Method for the removal of particulate matter and toxic compounds from engine exhaust, multifunctional filters and systems |
WO2018224651A2 (en) * | 2017-06-09 | 2018-12-13 | Basf Se | Catalytic article and exhaust gas treatment systems |
KR102698126B1 (en) * | 2017-06-09 | 2024-08-27 | 바스프 코포레이션 | Catalytic article and exhaust gas treatment systems |
CN107803113A (en) * | 2017-12-15 | 2018-03-16 | 江苏龙净科杰催化剂再生有限公司 | The preparation method of flue gas ash removal denitration Tuo bioxin integrated ceramic filters |
EP3533510A1 (en) | 2018-02-28 | 2019-09-04 | Infuser IP ApS | An exhaust gas treatment method and system arranged for treating exhaust gases |
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EP3730210A1 (en) | 2019-04-26 | 2020-10-28 | Umicore Ag & Co. Kg | Catalyst ceramic candle filter for combined particulate removal and the selective catalytic reduction (scr) of nitrogen-oxides |
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JPH03130522A (en) * | 1989-10-12 | 1991-06-04 | Mitsubishi Heavy Ind Ltd | Diesel engine exhaust gas processor |
WO1998003249A1 (en) * | 1996-07-22 | 1998-01-29 | Fls Miljø A/S | Flue gas cleaning device with catalytic ceramic filter |
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DK3271049T3 (en) | 2015-03-20 | 2020-04-27 | Haldor Topsoe As | Catalyzed ceramic core filter and process for purifying process flue gas or exhaust gas |
US10105682B2 (en) * | 2015-03-20 | 2018-10-23 | Haldor Topsøe A/S | Catalyzed ceramic candle filter and method for cleaning of off- or exhaust gases |
KR102454125B1 (en) | 2015-03-20 | 2022-10-14 | 토프쉐 에이/에스 | Catalyzed Ceramic Candle Filters and Methods for Purification of Process Offgases or Exhaust Gases |
-
2015
- 2015-03-20 US US15/545,499 patent/US10105682B2/en active Active
- 2015-03-20 JP JP2017546964A patent/JP6571788B2/en active Active
- 2015-03-20 WO PCT/EP2015/055952 patent/WO2016150465A1/en active Application Filing
- 2015-03-20 CA CA2976131A patent/CA2976131C/en active Active
- 2015-03-20 CN CN201580077976.1A patent/CN107427771B/en active Active
- 2015-03-20 EP EP15711179.0A patent/EP3271050A1/en not_active Withdrawn
- 2015-03-20 KR KR1020177021030A patent/KR102424112B1/en active IP Right Grant
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2016
- 2016-03-10 AR ARP160100631A patent/AR103898A1/en unknown
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JP6571788B2 (en) | 2019-09-04 |
EP3271050A1 (en) | 2018-01-24 |
US10105682B2 (en) | 2018-10-23 |
AR103898A1 (en) | 2017-06-14 |
JP2018514367A (en) | 2018-06-07 |
CN107427771A (en) | 2017-12-01 |
CN107427771B (en) | 2021-07-02 |
CA2976131A1 (en) | 2016-09-29 |
US20180008964A1 (en) | 2018-01-11 |
KR102424112B1 (en) | 2022-07-25 |
KR20170128220A (en) | 2017-11-22 |
WO2016150465A1 (en) | 2016-09-29 |
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